Location via proxy:   [ UP ]  
[Report a bug]   [Manage cookies]                
SlideShare a Scribd company logo

1

International Journal of Trend in Scientific Research and Development (IJTSRD)
Volume 5 Issue 4, May-June 2021 Available Online: www.ijtsrd.com e-ISSN: 2456 – 6470
@ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1568
A Review on Study of Heat Transfer
Analysis of Helical Coil Heat Exchangers
Atul Vats, Sunil Kumar Chaturvedi, Abhishek Bhandari
Department of Mechanical Engineering, NRI Institute of Research and Technical, Bhopal, Madhya Pradesh, India
ABSTRACT
Now a day’s a geometrically modified Helical coil heat exchangers are widely
using in industrial applications like cryogenic state processes, air-
conditioning, thermal nuclear reactors and waste heat recovery due to their
compact size and high heat transfercoefficient.Advantage ofusinghelical coils
over straight tubes is that the residence time spread is reduced, allowing
helical coils to be used to reduce axial dispersion in tubular reactors. In this
study, numerical investigationoftheinfluenceofgeometrical parameterssuch
as tube diameter (d), coil radius(R), and coil pitch(p) on overall heat transfer
coefficient in helical double tube heat exchangers are performed using a
professional CFD software- FLUENT. In recent years, numerous styles were
introduced for heat exchangersthatapplytocompletely differentapplications;
sadly, their heat transfer co-efficient wasn't reliable at different operational
conditions. the standard of the heat changed rate wasn't optimized and there
have been many deficiencies and errors in styles. The heat transfer of the
copper material is enhanced in comparison with other material unfortunately
thermal resistance is reduced with an increase in pressure drop thus
enhancing the heat transfer ontheheatexchanger.Helical architectureisoften
designed with a clear motive of compact size and also address heat transfer
co-efficient and other ancillary attributes efficiently and effectively. So the
better material is suggested for an industrial heat exchanger according to the
applications is Copper with the basis of simulation results. The geometry and
different dimension parameter ofthehelical coil showthattheproposedstudy
in different material properties and different mass flow rates to heat transfer
are maximum in different parameter helical coil heat exchangers. Finally, the
heat transfer increase for the copper material compared to another material
but with the increase in pressure drop the corresponding thermal resistance
decreases which allow the improved heat transfer rate and the rate increases
from Aluminum to Bronze to Copper. With the drop in temperature, the
thermal resistance is reduced which enhances the heat transfer rate. The
simulation results show that the copper has a high heat transfer coefficient
than Aluminum and Bronze while operating in identical conditions.Duetothe
extensive use of helical coils in various applications,knowledgeabouttheflow
patterns and heat transfer characteristics are important.
KEYWORDS: Heat Exchanger, Helical Coil, Heat Transfer, CFD, Heat transfer
Coefficient, Pressure Drop
How to cite this paper: Atul Vats | Sunil
Kumar Chaturvedi|Abhishek Bhandari"A
Review on Study of Heat Transfer
Analysis of Helical Coil Heat Exchangers"
Published in
International Journal
of Trend in Scientific
Research and
Development(ijtsrd),
ISSN: 2456-6470,
Volume-5 | Issue-4,
June 2021, pp.1568-
1572, URL:
www.ijtsrd.com/papers/ijtsrd43650.pdf
Copyright © 2021 by author (s) and
International Journal ofTrendinScientific
Research and Development Journal. This
is an Open Access article distributed
under the terms of
the Creative
Commons Attribution
License (CC BY 4.0)
(http: //creativecommons.org/licenses/by/4.0)
I. INTRODUCTION
Exchanging Heat is an operation wherever in the heat is
transferred from mass of one fluid to another fluid that is
often exploited in heating and cooling based mostly on the
operation throughout the globe. In a typical sense,a deviceis
outlined as a convenience or mechanical setup utilized for
the procedure of warmth trades between two or a lot of
liquids that area unit at varying temperatures.. Heat
exchangers area unit valuable in various planning
procedures such as folks with important influence plants,
refrigerant and aerating and cooling frameworks, power
frameworks, conservative device atomic force plants,
nourishment getting ready plants, concoction reactors,
HVAC, house, and aeronautical applications The most
commonly used type of HE is the shell and tube heat
exchanger. In the present study, a comparative analysis of a
water to water Shell & Tube HE wherein, hot water flows
inside the tubes and cold water inside the shell is made, to
study and analyze the heat transfer coefficient and pressure
drops for different mass flow rates and inlet and outlet
temperatures Bell Delaware methods.
OBJECTIVES: The criterion of any heat exchanger is to
develop in a manner of maximum transformation of heat
from hot fluid to cold fluid in a plant in order to eliminate
wastages of heat in effective ways. Design and development
of heat exchangers are based on heat transfer per unit area
where as some space is required and are modeled with
respect to availability of space to install it. This project will
help to understand and will provide CFD solution, at
different aspects parameter through flow of fluid on
differently constructed material of helical type heat
exchanger which improve efficiency. The transfer of heat to
and from process fluids is an essential part of most of the
IJTSRD43650

2

International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1569
chemical processes. Therefore, heat exchangers are used
extensively and regularly in process and allied industries
and are very important during design and operation.
In the present study, a comparative analysiswill bedoneofa
water to water Spiral HE wherein, hot water flowsinsidethe
tubes and cold water inside the shell is made. The heat
transfer coefficient and pressure drops for fixed mass flow
rates and inlet and outlet temperature by using Fluent 14.0
(CFD) will analyzed.
Main Objectives are:
To Analyze and Design the Spiral heat exchanger for
various given material.
To Calculate the Heat Transfer for various material and
To compare the heat transfer characteristic between
Copper, Bronze and metal on various working
parameter by using Fluent14.0.
II. LITERATURE REVIEW
The first steps towards the getting an ideas to do some
conceptual change in design and analysis as it is require,
literature review done , taken as a references and found
some useful decision making in the form conclusion and
report are in the form of their descriptive summary below.
J.S. Jayakumaret. al [1] presented the effects of the fixed
thermal and transfer properties of the system on estimation
of the heat transfer coefficients. The CFD based
experimentation analysis show that estimatedco-efficientis
within the permissible range of real-time scenario and the
correlation between the two was also presented.
Usman Ur Rehman [2] studied the heat transfer and flow
distribution in a shell and tube heat exchanger and
compared them with the experimental results. The model
showed an average error of around 20% in the heat transfer
and the pressure difference.
Nawras H. et.al [3] illustrated the performance of elliptical
tubes based on the mechanical and thermal parameters
employed for polymer heat exchangers. The mechanical
analysis proves that the streamlined shape of the outer tube
had an optimal thermal performance based on analysis over
different geometries of the tube and materials.
K. Abdul Hamid et. al. [4] has done work on pressure drop
for Ethylene Glycol (EG) based nano fluid. The nano fluid is
prepared by dilution technique of TiO2 in based fluid of
mixture water and EG in volume ratio of 60:40, at three
volume concentrations of 0.5 %, 1.0 % and 1.5 %. The
experiment was conducted under a flow loop with a
horizontal tube test section at various values of flow rate for
the range of Reynolds number less than 30,000. The
experimental result of TiO2 nano fluid pressure drop is
compared with the Blasius equation for based fluid. It was
observed that pressure drop increase with increasing of
nano fluid volume concentration and decrease with
increasing of nano fluid temperature insignificantly. He
found that TiO2 is not significantly increased compare to EG
fluid. The working temperature of nano fluid will reduce the
pressure drop due to the decreasing in nano fluid viscosity.
Shiva Kumar et. al [5] have worked on both straight tube
and helical tube heat exchanger. He has compared CFD
results with the results obtained by the simulation of
straight tubular heat exchanger of the same length under
identical operating conditions. Results indicated that helical
heat exchangers showed 11% increase in the heat transfer
rate over the straight tube. Simulation results also showed
10% increase in nusselt number for thehelical coilswhereas
pressure drop in case of helical coils is higher when
compared to the straight tube.
Hemasunder Banka et. al. [6] has done an analytical
investigation on the shell and tube heat exchanger using
forced convective heat transfer to determine flow
characteristics of nano fluids by varying volume fractions
and mixed with water , the nano fluids are titanium carbide
(TiC), titanium nitride (TiN) andZnOnanofluidanddifferent
volume concentrations (0.02, 0.04, 0.07 & 0.15%) flowing
under turbulent flow conditions. CFD analysis is done on
heat exchanger by applying the properties of nanofluidwith
different volume fractions to obtain temperature
distribution, heat transfer coefficient and heat transfer rate.
He found that heat transfer coefficient and heat transfer
rates are increasing by increasing the volume fractions.
Daniel Flórez-Orrego et.al [7] bestowed a detail study on
flow and therefore the heat transfer over a device designed
supported cone formed helical coil. The simulations result
shows similarities within the elements related to rate
contours of thewarmthexchanger.moreover,deviations and
errors within the analysis werefoundowingtounevenflame
radiation with a deviation around twenty third was
recorded. The reliable correlation with the nusselt range
values shows that the design provide improved
performance.
Timothy J. Rennie [8] studied each parallel and counter
fluid flows in cycle for heat exchanger designed supported
double pipe coiling frame work with a scope of warmth
transfer characteristics associated. The simulation analysis
proves thatthe overall heat transfer constants is directly
proportional to the inner dean range however the fluid flow
conditions within the outer pipe had a serious contribution
on the general heat transfer coefficient.
Usman ur Rehman [9] studied the heat transfer and flow
distribution during a shell and tube device and compared
them with the experimental results. The model showed a
mean error of around two hundredth within the heat
transfer and therefore the pressure distinction.
Nawras H. et.al [10] illustratedtheperformanceofelliptical
tubes supported the mechanical and thermal parameters
used for chemical compound heat exchangers. The
mechanical analysis proves that the efficient form of the
outer tube had an best thermal performance supported
analysis over completely different geometries of the tube
and materials.
Tuckerman and Pease [11] exploited silicon micro-
channels, with water becausetheoperatingfluid,todissipate
power from an electronic chip. The micro-channels were
engraved {during a in an exceedingly in a very} atomic
number 14 sample with an overall dimension of 1cm2. The
tiny characteristic length scale of silicon small channels
prompted the scientific community to analyze the chance of
new transport physics.
III. METHODOLOGY
Descriptive analysisthat'sfindingfactsandsurveys,whereas
applied and elementary analysis aims to seek out a
resolution to social issues or industrial issues. There are
primarily two varieties of analysis approach that's a
quantitative and qualitative analysis

3

International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1570
These are is more subdivided into experimental and
simulation approaches. The experimental approaches are
characterized with larger control over the atmosphere
whereas simulation approaches it includesthedevelopment
artificial atmosphere at intervals that relevant info and
knowledge may be generated, during this project, a
comparative analysis of helical device with totally different
material using machine Fluid Dynamic (CFD) are done. The
comparative analysis is completed in terms of style contour
variations and flow of fluid Transmit. The below fig.1
showing the step by step procedure on Ansys CFD and on
applying relevant boundary condition result may be
analyzed and simulation of fluid flow will be done.
Fig.1 Steps involved in CFD
The step considered on Fluent as an important phase that
determines the constraint imposed by the environment,
application or other over the heat transfer requirement and
performance. In addition, the problem type and physical
model are vital constraint variables that determine the
robustness of the heat exchanger as discussed in Ansys
fluent 14.0 are namely
Type – Solid (3D)
Scope – Operational Pressure
Model – Turbulence framework with twin expressions
FLUID PROPERTY: - The current factor incorporated as a
boundary condition is the subjective and alters with
reference to the material and fluid properties in
consideration as presented in given table 1& 2 below.
Table No.1
Types of Fluid Water
Density 998.2kg3/m
Viscosity .0010003kg/m3
Specific Heat 4182jule/g.kal
Thermal Conductivity 0.6 watt/kal
Table No.2
Temperature 332K
Mass flow rate (Different) 0.02kg/s
Turbulence intensity ratio .5%
Turbulence viscosity ratio 10%
Wall temperature 293k
Outlet Pressure outlet
Operating condition pressure 101325Pa
IV. RESULT AND DISCUSSION
We firmly believe in the theory that every Joule (energy not
used) lost means every Joule (energy needs to be produced)
generate which in developing countries like India with ever
increasing power demand could mount to significant socio-
economic and environmental losses. In this thesis, we
illustrated the need for heat exchangers that could offer a
high heat transfer co-efficient that exploits coil’s highly
complex design based on helical architectures. Furthermore,
a comparative analysis of the helical design of the coil with
different materials (like Aluminum, Bonze, and Copper) and
different flow rates was presented.
It well-documented fact thatvariousdesignimplementations
of the coils has been introduced with inlet and outlet for the
flow of the fluid. The important feature of the thesis is to
provide a comprehensive analysis of the product life of the
cycle associated with a heat exchanger in terms of material,
pressure temperature, thermal conductivity, maximum heat
transfer rate, and design. The heat transfer of the copper
material is enhanced in comparison with other material
unfortunately thermal resistance is reducedwithanincrease
in pressure drop thus enhancing the heattransferontheheat
exchanger. Helical architecture is often designed with a clear
motive of compact size and also addresses heat transfer co-
efficient and other ancillary attributes efficiently and
effectively. So the better material is suggested for an
industrial heat exchanger according to the applications is
Copper with the basis of simulation results.
Simulation results show that while we go to the different
materials pressure drop is increasing from Aluminum to
Bronze and Bronze to Copper and Temperature drop is
decreases so the thermal resistance is decreased hence the
heat transfer rate is also increased. Heat transfer coefficient,
pressure drop and corresponding rate are higher in case of
Copper in identical conditions. Also the comparisonbetween
different material and different mass flow rate are also
studied. The geometry and different dimension parameterof
helical coil shows that proposed study in different material
properties and different mass flow rate to heat transfer is
maximum in different parameter helical coil heat exchanger.
Finally, the heat transfer increase for the copper material
compared to another material but with increase in pressure
drop the corresponding thermal resistance decreases which
allows the improved heat transfer rate and therateincreases
from Aluminum to Bronze to Copper. With the drop in
temperature the thermal resistance is reduced which

4

International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1571
enhances the heat transferrate.Thesimulationsresultsshow
that the copper has high heat transfer co-efficient than
Aluminum and Bronze while operating in identical
conditions. Method for solving CFD analysis of helical coil
heat exchanger would be carried out using “ANSYS 14.0”
while the feasibility of model is analyzed via CAD model
Generation of 3D model by using “Catia ver 5.0”.
V. CONCLUSION
It is possible with helical coil heat exchanger to transferheat
at a faster rate compare to other type of heat exchanger. On
simulating the results as per defined value of boundary
condition in CFD it will shows that while going to adopt the
different materials, being all materials have specific thermal
.roperties? Pressure drop will increase from Aluminum to
Bronze and Bronze to Copper and Temperature drop is
decreases so the thermal resistance is decreased hence the
heat transfer rate is also increased. Heat transfer coefficient,
pressure drop and corresponding rate are higher in case of
Copper in identical conditions.Alsothecomparison between
different material and different mass flow rate are also
studied. The designed geometry and different dimension
parameter of helical coil shows that proposed study in
different material properties anddifferentmassflowrate the
heat transfer is maximum in different parameter helical coil
heat exchanger. Finally, the heat transfer increase for the
copper material compared to another material but with
increase in pressure drop the corresponding thermal
resistance decreases which allows the improved heat
transfer rate and the rate increases from Aluminum to
Bronze to Copper. With the drop in temperaturethethermal
resistance is reduced which enhances the heat transfer rate.
The simulations results show that the copper has high heat
transfer co-efficient than Aluminum and Bronze while
operating in identical conditions.
VI. FUTURE SCOPE
In an engineeringtransformationisnecessaryevensomehow
possible to modification in existing oneandtakingadvantage
of the possible feasible solution. The present study can be
extended by taking the following variables:-
1. Investigation can be done with a mass flow rate.
2. Study with different geometrical parameter like PCD,
Pitch and Pipe dia.
Comparison with different Velocity inlet
REFRENCE
[1] J. S. Jayakumar, S. M. Mahajani, J. C. Mandal, P. K.
Vijayan, and RohidasBhoi “Experimental and CFD
estimation of heat transfer in helically coiled heat
exchangers” 2008, Chemical Engineering Research
and Design 221-232.
[2] Usman Ur Rehman “Heat Transfer Optimization of
Shell-and-Tube Heat ExchangerthroughCFDStudies”
2011, Chalmers University of Technology.
[3] Nawras H. Mostafa, Qusay R.Al-Hagag“Structural and
Thermal Analysis of Heat Exchanger with Tubes of
Elliptical Shape” IASJ, 2012, Vol-8 Issue-3.
[4] K. Abdul Hamid, W. H. Azmi, RIzalman Mamat, N. A.
Usri and Gohalamhassan Najafi 2015, “Effect of
Titanium Oxide Nanofluid Concentration onPressure
drop” ARPN Journal of Engineering and Applied
Sciences, Volume 10, Page 7815-7820.
[5] Shiva Kumar, K Vasudev Karanth 2013, “Numerical
analysis of a Helical CoiledHeatExchangerusingCFD”
International Journal of Thermal Technologies,
Volume 3, Page 126-130.
[6] Hemasunder Banka, Dr. V. Vikram Reddy, M. Radhika
2016, “CFD AnalysisofShell andTubeHeatExchanger
using Titanium Carbide, Titanium Nitride and Zinc
Oxide Nanofluid” International Journal ofInnovations
in Engineering and Technology, Special Issue, Page
315-322.
[7] Daniel Flórez-Orrego,“Experimental andCFDstudyof
a single phase cone- shaped helical coiled heat
exchanger: an empirical correlation” ECOS June 26-
29, 2012.
[8] Timothy John Rennie, “Numerical and Experimental
Studies of a Double pipe Helical Heat Exchanger”
Dept. of Bio-resource Engg. McGill University,
Montreal August 2004.
[9] Usman Ur Rehman “Heat Transfer Optimization of
Shell-and-Tube Heat ExchangerthroughCFDStudies”
2011, Chalmers University of Technology.
[10] Nawras H. Mostafa, Qusay R.Al-Hagag“Structural and
Thermal Analysis of Heat Exchanger with Tubes of
Elliptical Shape” IASJ, 2012, Vol-8 Issue-3.
[11] Tuckerman, D. B. and Pease, R. F. W., “High-
performance heat sinking for VLSI”, IEEE Electron
Device Letters, 1981
[12] Peng, X. F., Peterson, G. P., and Wang B. X., “Heat
transfer characteristics of water flowing through
micro channels”, Experimental Heat Transfer, 1994
[13] Peng, X. F. and Peterson, G. P., “Effect of thermo fluid
and geometrical parameters on convection of liquids
through rectangular micro-channels”, International
Journal of Heat and Mass Transfer, 1995, Vol. 38(4)
[14] Judy, J., Maynes, D., and Webb,B.W.,“Characterization
of frictional pressure dropfor liquid flows through
micro-channels”, International Journal of Heat and
Mass Transfer, 2002
[15] T. Srinivas, A. Venu Vinod 2015, “Heat Transfer
Enhancement using CuO/Water Nanofluid in a Shell
and Helical Coil Heat Exchanger” Elsevier, Volume
127, Page 1271-1277.
[16] Tushar A. Sinha, Amit Kumar, NikhileshBhargava and
Soumya S Mallick 2014, “An Experimental
Investigation into the Thermal Properties of Nano
Fluid” Applied Mechanical Engineering, Volume 4,
Issue 1.
[17] SadikKakaç and Hongtan Liu (2002). Heat
Exchangers: Selection, Rating and Thermal Design
(2nd ed.). CRC Press. ISBN 0-8493-0902-6.
[18] Saunders, E. A. (1988). Heat Exchanges: Selection,
Design and Construction. New York: Longman
Scientific and Technical. Industrial Shell-and-tube
heat exchangers; American Industrial Heat Transfer
Inc.; http://www.aihti.com/pdf/fbf.pdf.
[19] Kister, Henry Z. (1992). Distillation Design (1st ed.).
McGraw-Hill. ISBN 0- 07-034909-6.

5

International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1572
[20] Jump Perry, Robert H. and Green, Don W. (1984).
Perry's Chemical Engineers' Handbook (6th ed.).
McGraw-Hill. ISBN 0-07-049479-7.
[21] Air PollutionControl OrientationCoursefromwebsite
of the Air Pollution Training Institute Energy savings
in steam systems, Layout of surface condenser (scroll
to page 11 of 34 PDF pages)
[22] Coulson, J. & Richardson, J. (1983), Chemical
Engineering – Design (SI Units), Volume 6, Pergamon
Press, Oxford.
[23] Hewitt G, Shires G, Bott T (1994), Process Heat
Transfer, CRC Press Inc, Florida.
[24] John C Raisley, “MICROCHANNEL TECHNOLOGY”
Patent 2, 046, 968 issued July 7, 1936; filed Jan. 8,
1934.
[25] Kee, Robert J., et al. "The design, fabrication, and
evaluation of a ceramic counter-flow microchannel
heat exchanger. " AppliedThermal Engineering31.11
(2011): 2004-2012.
[26] David C. Denken berger, Michael J. Brand emuehl,
Joshua M. Pearce, and John Zhai, Expanded micro
channel heat exchanger: design, fabrication and
preliminary experimental test, Proceedings of the
Institution of Mechanical Engineers – PartA:Journalof
Power and Energy, 226, 532-544 (2012). DOI: 10.
1177/0957650912442781
[27] Northcutt, B., & Mudawar, I. (2012). Enhanced design
of cross-flow micro channel heat exchanger module
for high-performance aircraft gas turbine engines.
Journal of Heat Transfer, 134(6), 061801.
[28] Moallem, E., Padhmanabhan, S., Cremaschi, L., &
Fisher, D. E. (2012). Experimental investigationofthe
surface temperature and water retention effects on
the frosting performance of a compact micro channel
heat exchanger for heat pump systems. International
journal of refrigeration, 35(1), 171-186.
[29] Xu, B., Shi, J., Wang, Y., Chen, J., Li, F., & Li, D. (2014).
Experimental Study of Fouling Performance of Air
Conditioning System with Micro channel Heat
Exchanger.
[30] D. Denkenberger, M. Parisi, J. M. Pearce. Towards
Low-Cost Microchannel Heat Exchangers: Vehicle
Heat Recovery Ventilator Prototype. Proceedings of
the 10th International Conference on Heat Transfer,
Fluid Mechanics andThermodynamics(HEFAT),14–16
July 2014, Orlando, FL, USA.

More Related Content

A Review on Study of Heat Transfer Analysis of Helical Coil Heat Exchangers

  • 1. International Journal of Trend in Scientific Research and Development (IJTSRD) Volume 5 Issue 4, May-June 2021 Available Online: www.ijtsrd.com e-ISSN: 2456 – 6470 @ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1568 A Review on Study of Heat Transfer Analysis of Helical Coil Heat Exchangers Atul Vats, Sunil Kumar Chaturvedi, Abhishek Bhandari Department of Mechanical Engineering, NRI Institute of Research and Technical, Bhopal, Madhya Pradesh, India ABSTRACT Now a day’s a geometrically modified Helical coil heat exchangers are widely using in industrial applications like cryogenic state processes, air- conditioning, thermal nuclear reactors and waste heat recovery due to their compact size and high heat transfercoefficient.Advantage ofusinghelical coils over straight tubes is that the residence time spread is reduced, allowing helical coils to be used to reduce axial dispersion in tubular reactors. In this study, numerical investigationoftheinfluenceofgeometrical parameterssuch as tube diameter (d), coil radius(R), and coil pitch(p) on overall heat transfer coefficient in helical double tube heat exchangers are performed using a professional CFD software- FLUENT. In recent years, numerous styles were introduced for heat exchangersthatapplytocompletely differentapplications; sadly, their heat transfer co-efficient wasn't reliable at different operational conditions. the standard of the heat changed rate wasn't optimized and there have been many deficiencies and errors in styles. The heat transfer of the copper material is enhanced in comparison with other material unfortunately thermal resistance is reduced with an increase in pressure drop thus enhancing the heat transfer ontheheatexchanger.Helical architectureisoften designed with a clear motive of compact size and also address heat transfer co-efficient and other ancillary attributes efficiently and effectively. So the better material is suggested for an industrial heat exchanger according to the applications is Copper with the basis of simulation results. The geometry and different dimension parameter ofthehelical coil showthattheproposedstudy in different material properties and different mass flow rates to heat transfer are maximum in different parameter helical coil heat exchangers. Finally, the heat transfer increase for the copper material compared to another material but with the increase in pressure drop the corresponding thermal resistance decreases which allow the improved heat transfer rate and the rate increases from Aluminum to Bronze to Copper. With the drop in temperature, the thermal resistance is reduced which enhances the heat transfer rate. The simulation results show that the copper has a high heat transfer coefficient than Aluminum and Bronze while operating in identical conditions.Duetothe extensive use of helical coils in various applications,knowledgeabouttheflow patterns and heat transfer characteristics are important. KEYWORDS: Heat Exchanger, Helical Coil, Heat Transfer, CFD, Heat transfer Coefficient, Pressure Drop How to cite this paper: Atul Vats | Sunil Kumar Chaturvedi|Abhishek Bhandari"A Review on Study of Heat Transfer Analysis of Helical Coil Heat Exchangers" Published in International Journal of Trend in Scientific Research and Development(ijtsrd), ISSN: 2456-6470, Volume-5 | Issue-4, June 2021, pp.1568- 1572, URL: www.ijtsrd.com/papers/ijtsrd43650.pdf Copyright © 2021 by author (s) and International Journal ofTrendinScientific Research and Development Journal. This is an Open Access article distributed under the terms of the Creative Commons Attribution License (CC BY 4.0) (http: //creativecommons.org/licenses/by/4.0) I. INTRODUCTION Exchanging Heat is an operation wherever in the heat is transferred from mass of one fluid to another fluid that is often exploited in heating and cooling based mostly on the operation throughout the globe. In a typical sense,a deviceis outlined as a convenience or mechanical setup utilized for the procedure of warmth trades between two or a lot of liquids that area unit at varying temperatures.. Heat exchangers area unit valuable in various planning procedures such as folks with important influence plants, refrigerant and aerating and cooling frameworks, power frameworks, conservative device atomic force plants, nourishment getting ready plants, concoction reactors, HVAC, house, and aeronautical applications The most commonly used type of HE is the shell and tube heat exchanger. In the present study, a comparative analysis of a water to water Shell & Tube HE wherein, hot water flows inside the tubes and cold water inside the shell is made, to study and analyze the heat transfer coefficient and pressure drops for different mass flow rates and inlet and outlet temperatures Bell Delaware methods. OBJECTIVES: The criterion of any heat exchanger is to develop in a manner of maximum transformation of heat from hot fluid to cold fluid in a plant in order to eliminate wastages of heat in effective ways. Design and development of heat exchangers are based on heat transfer per unit area where as some space is required and are modeled with respect to availability of space to install it. This project will help to understand and will provide CFD solution, at different aspects parameter through flow of fluid on differently constructed material of helical type heat exchanger which improve efficiency. The transfer of heat to and from process fluids is an essential part of most of the IJTSRD43650
  • 2. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1569 chemical processes. Therefore, heat exchangers are used extensively and regularly in process and allied industries and are very important during design and operation. In the present study, a comparative analysiswill bedoneofa water to water Spiral HE wherein, hot water flowsinsidethe tubes and cold water inside the shell is made. The heat transfer coefficient and pressure drops for fixed mass flow rates and inlet and outlet temperature by using Fluent 14.0 (CFD) will analyzed. Main Objectives are: To Analyze and Design the Spiral heat exchanger for various given material. To Calculate the Heat Transfer for various material and To compare the heat transfer characteristic between Copper, Bronze and metal on various working parameter by using Fluent14.0. II. LITERATURE REVIEW The first steps towards the getting an ideas to do some conceptual change in design and analysis as it is require, literature review done , taken as a references and found some useful decision making in the form conclusion and report are in the form of their descriptive summary below. J.S. Jayakumaret. al [1] presented the effects of the fixed thermal and transfer properties of the system on estimation of the heat transfer coefficients. The CFD based experimentation analysis show that estimatedco-efficientis within the permissible range of real-time scenario and the correlation between the two was also presented. Usman Ur Rehman [2] studied the heat transfer and flow distribution in a shell and tube heat exchanger and compared them with the experimental results. The model showed an average error of around 20% in the heat transfer and the pressure difference. Nawras H. et.al [3] illustrated the performance of elliptical tubes based on the mechanical and thermal parameters employed for polymer heat exchangers. The mechanical analysis proves that the streamlined shape of the outer tube had an optimal thermal performance based on analysis over different geometries of the tube and materials. K. Abdul Hamid et. al. [4] has done work on pressure drop for Ethylene Glycol (EG) based nano fluid. The nano fluid is prepared by dilution technique of TiO2 in based fluid of mixture water and EG in volume ratio of 60:40, at three volume concentrations of 0.5 %, 1.0 % and 1.5 %. The experiment was conducted under a flow loop with a horizontal tube test section at various values of flow rate for the range of Reynolds number less than 30,000. The experimental result of TiO2 nano fluid pressure drop is compared with the Blasius equation for based fluid. It was observed that pressure drop increase with increasing of nano fluid volume concentration and decrease with increasing of nano fluid temperature insignificantly. He found that TiO2 is not significantly increased compare to EG fluid. The working temperature of nano fluid will reduce the pressure drop due to the decreasing in nano fluid viscosity. Shiva Kumar et. al [5] have worked on both straight tube and helical tube heat exchanger. He has compared CFD results with the results obtained by the simulation of straight tubular heat exchanger of the same length under identical operating conditions. Results indicated that helical heat exchangers showed 11% increase in the heat transfer rate over the straight tube. Simulation results also showed 10% increase in nusselt number for thehelical coilswhereas pressure drop in case of helical coils is higher when compared to the straight tube. Hemasunder Banka et. al. [6] has done an analytical investigation on the shell and tube heat exchanger using forced convective heat transfer to determine flow characteristics of nano fluids by varying volume fractions and mixed with water , the nano fluids are titanium carbide (TiC), titanium nitride (TiN) andZnOnanofluidanddifferent volume concentrations (0.02, 0.04, 0.07 & 0.15%) flowing under turbulent flow conditions. CFD analysis is done on heat exchanger by applying the properties of nanofluidwith different volume fractions to obtain temperature distribution, heat transfer coefficient and heat transfer rate. He found that heat transfer coefficient and heat transfer rates are increasing by increasing the volume fractions. Daniel Flórez-Orrego et.al [7] bestowed a detail study on flow and therefore the heat transfer over a device designed supported cone formed helical coil. The simulations result shows similarities within the elements related to rate contours of thewarmthexchanger.moreover,deviations and errors within the analysis werefoundowingtounevenflame radiation with a deviation around twenty third was recorded. The reliable correlation with the nusselt range values shows that the design provide improved performance. Timothy J. Rennie [8] studied each parallel and counter fluid flows in cycle for heat exchanger designed supported double pipe coiling frame work with a scope of warmth transfer characteristics associated. The simulation analysis proves thatthe overall heat transfer constants is directly proportional to the inner dean range however the fluid flow conditions within the outer pipe had a serious contribution on the general heat transfer coefficient. Usman ur Rehman [9] studied the heat transfer and flow distribution during a shell and tube device and compared them with the experimental results. The model showed a mean error of around two hundredth within the heat transfer and therefore the pressure distinction. Nawras H. et.al [10] illustratedtheperformanceofelliptical tubes supported the mechanical and thermal parameters used for chemical compound heat exchangers. The mechanical analysis proves that the efficient form of the outer tube had an best thermal performance supported analysis over completely different geometries of the tube and materials. Tuckerman and Pease [11] exploited silicon micro- channels, with water becausetheoperatingfluid,todissipate power from an electronic chip. The micro-channels were engraved {during a in an exceedingly in a very} atomic number 14 sample with an overall dimension of 1cm2. The tiny characteristic length scale of silicon small channels prompted the scientific community to analyze the chance of new transport physics. III. METHODOLOGY Descriptive analysisthat'sfindingfactsandsurveys,whereas applied and elementary analysis aims to seek out a resolution to social issues or industrial issues. There are primarily two varieties of analysis approach that's a quantitative and qualitative analysis
  • 3. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1570 These are is more subdivided into experimental and simulation approaches. The experimental approaches are characterized with larger control over the atmosphere whereas simulation approaches it includesthedevelopment artificial atmosphere at intervals that relevant info and knowledge may be generated, during this project, a comparative analysis of helical device with totally different material using machine Fluid Dynamic (CFD) are done. The comparative analysis is completed in terms of style contour variations and flow of fluid Transmit. The below fig.1 showing the step by step procedure on Ansys CFD and on applying relevant boundary condition result may be analyzed and simulation of fluid flow will be done. Fig.1 Steps involved in CFD The step considered on Fluent as an important phase that determines the constraint imposed by the environment, application or other over the heat transfer requirement and performance. In addition, the problem type and physical model are vital constraint variables that determine the robustness of the heat exchanger as discussed in Ansys fluent 14.0 are namely Type – Solid (3D) Scope – Operational Pressure Model – Turbulence framework with twin expressions FLUID PROPERTY: - The current factor incorporated as a boundary condition is the subjective and alters with reference to the material and fluid properties in consideration as presented in given table 1& 2 below. Table No.1 Types of Fluid Water Density 998.2kg3/m Viscosity .0010003kg/m3 Specific Heat 4182jule/g.kal Thermal Conductivity 0.6 watt/kal Table No.2 Temperature 332K Mass flow rate (Different) 0.02kg/s Turbulence intensity ratio .5% Turbulence viscosity ratio 10% Wall temperature 293k Outlet Pressure outlet Operating condition pressure 101325Pa IV. RESULT AND DISCUSSION We firmly believe in the theory that every Joule (energy not used) lost means every Joule (energy needs to be produced) generate which in developing countries like India with ever increasing power demand could mount to significant socio- economic and environmental losses. In this thesis, we illustrated the need for heat exchangers that could offer a high heat transfer co-efficient that exploits coil’s highly complex design based on helical architectures. Furthermore, a comparative analysis of the helical design of the coil with different materials (like Aluminum, Bonze, and Copper) and different flow rates was presented. It well-documented fact thatvariousdesignimplementations of the coils has been introduced with inlet and outlet for the flow of the fluid. The important feature of the thesis is to provide a comprehensive analysis of the product life of the cycle associated with a heat exchanger in terms of material, pressure temperature, thermal conductivity, maximum heat transfer rate, and design. The heat transfer of the copper material is enhanced in comparison with other material unfortunately thermal resistance is reducedwithanincrease in pressure drop thus enhancing the heattransferontheheat exchanger. Helical architecture is often designed with a clear motive of compact size and also addresses heat transfer co- efficient and other ancillary attributes efficiently and effectively. So the better material is suggested for an industrial heat exchanger according to the applications is Copper with the basis of simulation results. Simulation results show that while we go to the different materials pressure drop is increasing from Aluminum to Bronze and Bronze to Copper and Temperature drop is decreases so the thermal resistance is decreased hence the heat transfer rate is also increased. Heat transfer coefficient, pressure drop and corresponding rate are higher in case of Copper in identical conditions. Also the comparisonbetween different material and different mass flow rate are also studied. The geometry and different dimension parameterof helical coil shows that proposed study in different material properties and different mass flow rate to heat transfer is maximum in different parameter helical coil heat exchanger. Finally, the heat transfer increase for the copper material compared to another material but with increase in pressure drop the corresponding thermal resistance decreases which allows the improved heat transfer rate and therateincreases from Aluminum to Bronze to Copper. With the drop in temperature the thermal resistance is reduced which
  • 4. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1571 enhances the heat transferrate.Thesimulationsresultsshow that the copper has high heat transfer co-efficient than Aluminum and Bronze while operating in identical conditions. Method for solving CFD analysis of helical coil heat exchanger would be carried out using “ANSYS 14.0” while the feasibility of model is analyzed via CAD model Generation of 3D model by using “Catia ver 5.0”. V. CONCLUSION It is possible with helical coil heat exchanger to transferheat at a faster rate compare to other type of heat exchanger. On simulating the results as per defined value of boundary condition in CFD it will shows that while going to adopt the different materials, being all materials have specific thermal .roperties? Pressure drop will increase from Aluminum to Bronze and Bronze to Copper and Temperature drop is decreases so the thermal resistance is decreased hence the heat transfer rate is also increased. Heat transfer coefficient, pressure drop and corresponding rate are higher in case of Copper in identical conditions.Alsothecomparison between different material and different mass flow rate are also studied. The designed geometry and different dimension parameter of helical coil shows that proposed study in different material properties anddifferentmassflowrate the heat transfer is maximum in different parameter helical coil heat exchanger. Finally, the heat transfer increase for the copper material compared to another material but with increase in pressure drop the corresponding thermal resistance decreases which allows the improved heat transfer rate and the rate increases from Aluminum to Bronze to Copper. With the drop in temperaturethethermal resistance is reduced which enhances the heat transfer rate. The simulations results show that the copper has high heat transfer co-efficient than Aluminum and Bronze while operating in identical conditions. VI. FUTURE SCOPE In an engineeringtransformationisnecessaryevensomehow possible to modification in existing oneandtakingadvantage of the possible feasible solution. The present study can be extended by taking the following variables:- 1. Investigation can be done with a mass flow rate. 2. Study with different geometrical parameter like PCD, Pitch and Pipe dia. Comparison with different Velocity inlet REFRENCE [1] J. S. Jayakumar, S. M. Mahajani, J. C. Mandal, P. K. Vijayan, and RohidasBhoi “Experimental and CFD estimation of heat transfer in helically coiled heat exchangers” 2008, Chemical Engineering Research and Design 221-232. [2] Usman Ur Rehman “Heat Transfer Optimization of Shell-and-Tube Heat ExchangerthroughCFDStudies” 2011, Chalmers University of Technology. [3] Nawras H. Mostafa, Qusay R.Al-Hagag“Structural and Thermal Analysis of Heat Exchanger with Tubes of Elliptical Shape” IASJ, 2012, Vol-8 Issue-3. [4] K. Abdul Hamid, W. H. Azmi, RIzalman Mamat, N. A. Usri and Gohalamhassan Najafi 2015, “Effect of Titanium Oxide Nanofluid Concentration onPressure drop” ARPN Journal of Engineering and Applied Sciences, Volume 10, Page 7815-7820. [5] Shiva Kumar, K Vasudev Karanth 2013, “Numerical analysis of a Helical CoiledHeatExchangerusingCFD” International Journal of Thermal Technologies, Volume 3, Page 126-130. [6] Hemasunder Banka, Dr. V. Vikram Reddy, M. Radhika 2016, “CFD AnalysisofShell andTubeHeatExchanger using Titanium Carbide, Titanium Nitride and Zinc Oxide Nanofluid” International Journal ofInnovations in Engineering and Technology, Special Issue, Page 315-322. [7] Daniel Flórez-Orrego,“Experimental andCFDstudyof a single phase cone- shaped helical coiled heat exchanger: an empirical correlation” ECOS June 26- 29, 2012. [8] Timothy John Rennie, “Numerical and Experimental Studies of a Double pipe Helical Heat Exchanger” Dept. of Bio-resource Engg. McGill University, Montreal August 2004. [9] Usman Ur Rehman “Heat Transfer Optimization of Shell-and-Tube Heat ExchangerthroughCFDStudies” 2011, Chalmers University of Technology. [10] Nawras H. Mostafa, Qusay R.Al-Hagag“Structural and Thermal Analysis of Heat Exchanger with Tubes of Elliptical Shape” IASJ, 2012, Vol-8 Issue-3. [11] Tuckerman, D. B. and Pease, R. F. W., “High- performance heat sinking for VLSI”, IEEE Electron Device Letters, 1981 [12] Peng, X. F., Peterson, G. P., and Wang B. X., “Heat transfer characteristics of water flowing through micro channels”, Experimental Heat Transfer, 1994 [13] Peng, X. F. and Peterson, G. P., “Effect of thermo fluid and geometrical parameters on convection of liquids through rectangular micro-channels”, International Journal of Heat and Mass Transfer, 1995, Vol. 38(4) [14] Judy, J., Maynes, D., and Webb,B.W.,“Characterization of frictional pressure dropfor liquid flows through micro-channels”, International Journal of Heat and Mass Transfer, 2002 [15] T. Srinivas, A. Venu Vinod 2015, “Heat Transfer Enhancement using CuO/Water Nanofluid in a Shell and Helical Coil Heat Exchanger” Elsevier, Volume 127, Page 1271-1277. [16] Tushar A. Sinha, Amit Kumar, NikhileshBhargava and Soumya S Mallick 2014, “An Experimental Investigation into the Thermal Properties of Nano Fluid” Applied Mechanical Engineering, Volume 4, Issue 1. [17] SadikKakaç and Hongtan Liu (2002). Heat Exchangers: Selection, Rating and Thermal Design (2nd ed.). CRC Press. ISBN 0-8493-0902-6. [18] Saunders, E. A. (1988). Heat Exchanges: Selection, Design and Construction. New York: Longman Scientific and Technical. Industrial Shell-and-tube heat exchangers; American Industrial Heat Transfer Inc.; http://www.aihti.com/pdf/fbf.pdf. [19] Kister, Henry Z. (1992). Distillation Design (1st ed.). McGraw-Hill. ISBN 0- 07-034909-6.
  • 5. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD43650 | Volume – 5 | Issue – 4 | May-June 2021 Page 1572 [20] Jump Perry, Robert H. and Green, Don W. (1984). Perry's Chemical Engineers' Handbook (6th ed.). McGraw-Hill. ISBN 0-07-049479-7. [21] Air PollutionControl OrientationCoursefromwebsite of the Air Pollution Training Institute Energy savings in steam systems, Layout of surface condenser (scroll to page 11 of 34 PDF pages) [22] Coulson, J. & Richardson, J. (1983), Chemical Engineering – Design (SI Units), Volume 6, Pergamon Press, Oxford. [23] Hewitt G, Shires G, Bott T (1994), Process Heat Transfer, CRC Press Inc, Florida. [24] John C Raisley, “MICROCHANNEL TECHNOLOGY” Patent 2, 046, 968 issued July 7, 1936; filed Jan. 8, 1934. [25] Kee, Robert J., et al. "The design, fabrication, and evaluation of a ceramic counter-flow microchannel heat exchanger. " AppliedThermal Engineering31.11 (2011): 2004-2012. [26] David C. Denken berger, Michael J. Brand emuehl, Joshua M. Pearce, and John Zhai, Expanded micro channel heat exchanger: design, fabrication and preliminary experimental test, Proceedings of the Institution of Mechanical Engineers – PartA:Journalof Power and Energy, 226, 532-544 (2012). DOI: 10. 1177/0957650912442781 [27] Northcutt, B., & Mudawar, I. (2012). Enhanced design of cross-flow micro channel heat exchanger module for high-performance aircraft gas turbine engines. Journal of Heat Transfer, 134(6), 061801. [28] Moallem, E., Padhmanabhan, S., Cremaschi, L., & Fisher, D. E. (2012). Experimental investigationofthe surface temperature and water retention effects on the frosting performance of a compact micro channel heat exchanger for heat pump systems. International journal of refrigeration, 35(1), 171-186. [29] Xu, B., Shi, J., Wang, Y., Chen, J., Li, F., & Li, D. (2014). Experimental Study of Fouling Performance of Air Conditioning System with Micro channel Heat Exchanger. [30] D. Denkenberger, M. Parisi, J. M. Pearce. Towards Low-Cost Microchannel Heat Exchangers: Vehicle Heat Recovery Ventilator Prototype. Proceedings of the 10th International Conference on Heat Transfer, Fluid Mechanics andThermodynamics(HEFAT),14–16 July 2014, Orlando, FL, USA.